Subterranean Well Treatment Process

ABSTRACT

A process of treating a subterranean well comprising a plurality of flow channels and at least one of the flow channels is impaired. The treatment is used for alleviating the impairment. The process comprises a flow of gaseous carrier fluid supplied into the subterranean well. The gaseous carrier fluid pushes liquids out of the plurality of the flow channels. A liquid treatment agent is created. To create the liquid treatment agent, first, a surfactant solution is created and diluted with a solvent. The surfactant solution is created by compounding a plurality of non-ionic ethoxylated sorbitan fatty acid ester surfactants together until a proper hydrophilic-lipophilic balance is achieved. At some point, the liquid treatment agent is atomized. This atomized liquid treatment agent is blended with the gaseous carrier fluid, to create an atomized treatment fog. The atomized treatment fog is supplied into the subterranean well.

BACKGROUND

Subterranean wells, in particular withdrawal wells, gas wells, and injection wells that are used to extract crude oil or other various types of hydrocarbon materials, known as valuable liquids. Typically, these subterranean wells comprise a network of natural or manmade flow channels through which liquids and hydrocarbon materials enter into, before being extracted from the subterranean well for commercial purposes. As production time passes, these flow channels tend to get impaired by clogs. When enough flow channels become impaired, extraction levels of valuable liquids from the subterranean well diminish and ultimately make the subterranean well uneconomical. There is a need to treat a subterranean well by substantially alleviating clogs in the flow channels, so extraction levels of valuable liquids can return to optimal levels and allow the subterranean well to be economical again.

SUMMARY

A process of treating a subterranean well comprising a plurality of flow channels and at least one of the flow channels has been impaired. The treatment is used for alleviating the impairment. The process comprises, a continuous flow of gaseous carrier fluid supplied into the subterranean well. Once in the subterranean well, the gaseous carrier fluid substantially pushes liquids out of the plurality of the flow channels. At some point, a liquid treatment agent is created. To create the liquid treatment agent, first, a surfactant solution is created and diluted with a solvent. The surfactant solution is created by compounding a plurality of non-ionic ethoxylated sorbitan fatty acid ester surfactants together until a proper hydrophilic-lipophilic balance is achieved. At some point, the liquid treatment agent is atomized. This atomized liquid treatment agent is blended with the gaseous carrier fluid, to create an atomized treatment fog. The atomized treatment fog is supplied into the subterranean well.

A portion of the liquids can be removed from the bottom of the subterranean well before supplying the continuous flow of gaseous carrier fluid into the subterranean well. The atomized treatment fog can be pressurized while in the subterranean well. The pressurized atomized treatment fog can then remain in the subterranean well for a duration of time. After the duration of time has ended, the subterranean well is depressurized such that the volume of the atomized treatment fog can escape. The duration of time can be between three and seven days, but it does not have to be. A volume of the liquid treatment agent can be placed into a treatment supply tank. The liquid treatment agent can then be provided from the treatment supply tank to an atomizing apparatus. The atomizing apparatus can blend the atomized liquid treatment agent with the gaseous carrier fluid.

A sorbitan fatty acid ester can also be compounded with the surfactant solution until a proper hydrophilic-lipophilic balance is achieved. The liquid treatment agent can be enhanced by adding inorganic acids, organic acids, clay stabilizers, bactericides, scale inhibitors, dissolved salts, emulsion breakers, water block breakers, or corrosion inhibitors. The subterranean well process can be implemented through a gaseous carrier fluid atomizing system. The surfactant solution can be diluted with the solvent in a ratio of 1 part surfactant solution to 20 parts solvent. The solvent can be one of water, toluene, condensate, acetone, oils, mutual solvents, or a combination thereof. The gaseous carrier fluid can be air, natural gas, oxygen, propane, nitrogen, helium, carbon dioxide, or a combination thereof. The solution ratio of the atomized treatment fog can be between 100 and 400. The atomized treatment fog can have the ability to energize and reduce the viscosity of the valuable liquids in the subterranean well. The atomized treatment fog can be supplied into the subterranean well as an aerosol mist.

What is also presented is a process of treating a subterranean well comprising a plurality of flow channels and at least one of the flow channels has been impaired. The treatment is used for alleviating the impairment. The process comprises, a continuous flow of gaseous carrier fluid supplied into the subterranean well. Once in the subterranean well, the gaseous carrier fluid substantially pushes liquids out of the plurality of the flow channels. At some point, a liquid treatment agent is created. To create the liquid treatment agent, first, a compounded combination of surfactant solution and sorbitan fatty acid ester is created and then diluted with a solvent. The surfactant solution is created by compounding a plurality of non-ionic ethoxylated sorbitan fatty acid ester surfactants together. A sorbitan fatty acid ester can then be compounded with the surfactant solution until a proper hydrophilic-lipophilic balance is achieved. A volume of the liquid treatment agent is placed into a treatment supply tank. The liquid treatment agent is then provided from the treatment supply tank to an atomizing apparatus. The liquid treatment agent is atomized. This atomized liquid treatment agent is blended with the gaseous carrier fluid, to create an atomized treatment fog. The atomized treatment fog is supplied into the subterranean well as an aerosol mist. The atomized treatment fog is then pressurized while in the subterranean well. The pressurized atomized treatment fog remains in the subterranean well for a duration of time. After the duration of time has ended, the subterranean well is depressurized and the atomized treatment fog can escape.

A portion of the liquids can be removed from the bottom of the subterranean well before supplying the continuous flow of gaseous carrier fluid into the subterranean well. The duration of time can be between three and seven days, but it does not have to be. The liquid treatment agent can be enhanced by adding inorganic acids, organic acids, clay stabilizers, bactericides, scale inhibitors, dissolved salts, emulsion breakers, water block breakers, or corrosion inhibitors. The subterranean well process can be implemented through a gaseous carrier fluid atomizing system. The surfactant solution can be diluted with the solvent in a ratio of 1 part surfactant solution to 20 parts solvent. The solvent can be one of water, toluene, condensate, acetone, oils, mutual solvents, or a combination thereof. The gaseous carrier fluid can be air, natural gas, oxygen, propane, nitrogen, helium, carbon dioxide, or a combination thereof. The solution ratio of the atomized treatment fog can be between 100 and 400. The atomized treatment fog can have the ability to energize and reduce the viscosity of the valuable liquids in the subterranean well.

What is also presented is a process of treating contaminated portions of the earth with a surfactant solution. This process comprises creating surfactant solution by compounding a non-ionic ethoxylated sorbitan fatty acid ester surfactant with another surfactant until a proper hydrophilic-lipophilic balance is achieved. The surfactant solution is pressured into the contaminated portions of the earth. The surfactant solution energizes and reduces the viscosity of the contaminants in the contaminated portions of the earth. The contaminants treated with the surfactant solution are removed from the portions of the earth.

Those skilled in the art will realize that this invention is capable of embodiments that are different from those shown and that details of the devices and methods can be changed in various manners without departing from the scope of this invention. Accordingly, the drawings and descriptions are to be regarded as including such equivalent embodiments as do not depart from the spirit and scope of this invention.

BRIEF DESCRIPTION OF DRAWINGS

For a more complete understanding and appreciation of this invention, and its many advantages, reference will be made to the following detailed description taken in conjunction with the accompanying drawings.

FIG. 1 shows a side view of a subterranean well in its environment and a gaseous carrier fluid treatment apparatus used in conjunction therewith, the drawing being partially in schematic representation form.

DETAILED DESCRIPTION

Referring to the drawings, some of the reference numerals are used to designate the same or corresponding parts through several of the embodiments and figures shown and described. Corresponding parts are denoted in different embodiments with the addition of lowercase letters. Variations of corresponding parts in form or function that are depicted in the figures are described. It will be understood that variations in the embodiments can generally be interchanged without deviating from the invention.

Deep below the earth's surface, petroleum bearing formations contain liquids (valuable liquids such as, but not limited to, crude oil and other non-valuable liquids such as, but not limited to, brine water). Subterranean wells are drilled deep enough through the earth surface to reach the petroleum bearing formation. A plurality of natural or manmade interstitial flow channels (also known as a “fracture network”) exist or are created deep in the subterranean well. These flow channels enable valuable liquids to flow into the subterranean well through the effects of gravity and/or pressure from the petroleum bearing formation. After flowing into the subterranean well, the valuable liquids are extracted through the implementation of a pump jack.

Usually the petroleum bearing formation that surrounds the subterranean well is situated around 750 feet in depth below the earth and is approximately 20 feet in size from top to bottom. A plurality of subterranean wells can be drilled to access the valuable liquids in a single petroleum bearing formation. However, since each subterranean well is positioned at a different location, the petroleum bearing formation surrounding a specific subterranean well can be situated at a different depth, can be a different size, and have different specific characteristics.

As production time passes, the flow channels tend to become clogged and impaired by particles and/or swelled clays, which include, but are not limited to, scales, paraffins, asphaltenes, precipitating minerals, organic deposition, water block, emulsion block, and or the swelling of clays. These particles and/or swelled clays tend to allow more non-valuable liquids that are less viscous than the valuable liquids to flow through the flow channels. In turn, the proportion of non-valuable liquids begin to outweigh the amount of valuable liquids being produced from the subterranean well. After a long-enough duration, the proportion of non-valuable liquids over valuable liquids is so great that the subterranean well becomes uneconomical.

It is at this point that the subterranean well treatment process is implemented to alleviate impairment by particles and/or swelled clays, making the subterranean well economical again. As shown in FIG. 1, subterranean wells 14 are drilled through the earth 40 and into petroleum bearing formations 36 with the expectation that valuable liquids will flow into the subterranean well 14 for extraction. The subterranean well 14 is typically installed with a well casing 24 which provides structural integrity and allows the subterranean well 14 to be sealed. A well pump 12, which is typically a submersible pump of some kind, is installed at the bottom of the subterranean well 14. A pump jack 10 acts on the well pump 12 to remove valuable liquids and invaluable liquids through extraction piping 42 to production fluid tanks 44 on the surface.

A gaseous carrier fluid atomizing system 16 is installed on the subterranean well 14. The gaseous carrier fluid atomizing system 16 comprises an aerating pipe 20 that is connected to an atomizing apparatus 22. The atomizing apparatus 22 is in turn connected to a compressor 30 and a liquid pump 32. The liquid pump 32 is connected to a treatment supply tank 34, which contains a quantity of liquid treatment agent (discussed below). In this embodiment, the liquid pump 32 is a high-pressure pump. The gaseous carrier fluid atomizing system 16 is connected to the subterranean well 14 by connecting the distal end of an aerating pipe 20 to the head of the casing 28 of the subterranean well 14. A valve 26 is mounted on the aerating pipe 20.

In order to begin the treatment process, the pump jack 10 begins acting on the well pump 12 and substantially removes as much of the fluids from the bottom of the subterranean well 14 as possible. The compressor 30 then supplies pressurized gaseous carrier fluid through the aerating pipe 20 and down into the subterranean well 14. Once in the subterranean well 14, the gaseous carrier fluid pushes out any remaining liquids and enters into the flow channels 18.

To push out the remaining liquids, the compressor 30 creates a continuous and consistent flow of the gaseous carrier fluid into the subterranean well 14 with enough force to cause the liquids to retreat back through the flow channels 18 and into the petroleum bearing formation 36. The volume and pressure of the gaseous carrier fluid depends on both the specific characteristics of the petroleum bearing formation 36 surrounding the subterranean well 14 and the characteristics of the flow channels 18. Typically, a minimum of 10,000 cubic feet of gaseous carrier fluid is used in this process. Since gases can more quickly and easily enter areas that liquids cannot, it should be understood that implementing a gaseous carrier fluid is much more efficient than implementing carrier fluid in a liquid state. For economical purposes, the gaseous carrier fluid is either air or natural gas. However, other active gasses, such as oxygen or propane, or inactive gasses such as nitrogen, helium, or carbon dioxide, or a combination thereof can be used.

Once a continuous flow of gaseous carrier fluid has been established within the flow channels 18, the liquid pump 32 is operated and begins forcing the liquid treatment agent from the treatment supply tank 34 into the atomizing apparatus 22. The atomized liquid treatment agent then enters the aerating pipe 20 and blends with the gaseous carrier fluid to create an atomized treatment fog 38 that is misted as an aerosol into the subterranean well 14. Once misted as an aerosol, the atomized treatment fog 38 has a low enough viscosity to enable it to enter the petroleum bearing formation 36 and disperse through the smallest of the flow channels 18. The low viscosity of the atomized treatment fog 38 also allows it to coat all surfaces deep down in the subterranean well 14. In this embodiment, the blending of the liquid treatment agent with the gaseous carrier fluid is conducted through the atomizing apparatus 22. However, other apparatuses may be used to atomize the liquid treatment agent with the gaseous carrier fluid, so long as these apparatuses are properly suited to produce adequate atomized treatment fog 38.

The atomizing apparatus 22 has an internal nozzle (not shown) that finely atomizes the liquid treatment agent when high pressure is used to spray the liquid treatment agent out of the internal nozzle. The internal nozzle properly and evenly mists the liquid treatment agent with the gaseous carrier fluid that is flowing through the atomizing apparatus 22. After being misted, the flow of the gaseous carrier fluid causes the liquid treatment agent to be suspended and carried as the atomized treatment fog 38. If there was no flow of the gaseous carrier fluid or if the flow is improperly weak, the molecular attraction of certain molecules in the atomized liquid treatment agent would cause the molecules to come back together and the liquid treatment agent to stop being atomized.

The liquid treatment agent is chemically compounded to produce minimal amounts of foam when atomized. In turn, the atomized treatment fog 38 can be properly misted as an aerosol into the subterranean well 14 without foaming. This enables the atomized treatment fog 38 to have maximum penetration when entering the flow channels 18 and enabling full effectiveness of the treatment process. In this embodiment, the liquid pump 32 should begin its operations once the continuous and consistent flow of gaseous carrier fluid has been established into the flow channels 18.

It should be noted that in the past, other processes would incorporate various treatment agents comprising surfactants that foamed immediately after being misted as an aerosol. After foaming, the treatment agents then made contact with the flow channels 18. Foaming surfactants tend to create air bubbles within the flow channels 18 that block the subsequent flow of other fluids or treatment agent into the flow channels 14. In turn, this foaming effect reduces the ability of the treatment agent to enter into the flow channels 14 and be fully effective.

A multi-step process is used in creating the liquid treatment agent. In the first step, a surfactant solution is created by compounding a plurality of surfactants together. Through empirical testing, it has been found that the surfactant solution must comprise at least two non-ionic ethoxylated sorbitan fatty acid esters. In some instances, additional effectiveness has been found when a sorbitan fatty acid ester is compounded in with this plurality of non-ionic ethoxylated sorbitan fatty acid esters. These surfactants must be compounded together until a proper hydrophilic-lipophilic balance (HLB) is achieved that matches the specific characteristics of the petroleum bearing formation 36 surrounding the subterranean well 14. A surfactant solution having an HLB between 2 and 16 can be chosen to treat a subterranean well 14. In environments comprising shallow sands around the subterranean well 10, typically, a surfactant solution having an HLB of approximately 11.625 will suffice. It should be understood, HLB is considered the measure of the degree to which the surfactant is hydrophilic or lipophilic. It should also be understood prior processes do not blend surfactants in their treatment agents to match the specific HLB of the petroleum bearing formation 36 surrounding the subterranean well 14 to be treated.

In the second step, the surfactant solution is diluted with a solvent to create the liquid treatment agent. Usually the surfactant solution is diluted in the ratio of 1 part surfactant solution to 20 parts solvent (e.g. adding 5 gallons of the surfactant solution to 95 gallons of solvent). The solvent can be, but is not limited to, water, toluene, condensate, acetone, oils, mutual solvents, or a combination of any of these. It should be understood that inorganic acids, organic acids, clay stabilizers, dissolved salts, bactericides (including ionized metals), scale inhibitors, emulsion breakers, water block breakers, or corrosion inhibitors can further enhance the liquid treatment agent solution. It has been found that a minimum of 10 gallons of liquid treatment agent should be used in the process.

Through empirical testing it has been found that non-ionic ethoxylated sorbitan fatty acid esters have the unique ability to trap and hold the atomized treatment fog 38 in the valuable liquids. These non-ionic ethoxylated sorbitan fatty acid esters also seem to energize the valuable liquids while reducing their viscosity. This effect in turn allows the valuable liquids to flow from the flow channels with less resistance from entering the subterranean well 14. Non-ionic ethoxylated sorbitan fatty acid esters used in the surfactant solution are sometimes sold under the trademark TWEEN. Empirical testing has shown that surfactant solutions comprising TWEEN 65, TWEEN 80, and/or TWEEN 85 are particularly effective in trapping and holding the atomized treatment fog 38 in the valuable liquids. Sorbitan fatty acid esters that are used in the surfactant solution are sometimes sold under the trademark SPAN.

As mentioned above, the atomized liquid treatment agent and gaseous carrier fluid are misted together to create the atomized treatment fog 38. The relationship between the volume of gaseous carrier fluid and atomized liquid treatment agent is defined as the solution ratio. Through empirical testing it has been found solution ratios of 100 to 400 are very effective on an average sized subterranean well 14. In shallow subterranean wells 14, solution ratios of 160, comprising 16,000 cubic feet of gaseous carrier fluid with 100 gallons of liquid treatment agent, have been found to be very effective. However, it has been found that any solution ratio between 40 and 1,000 can be used in this process. For example, an embodiment of the process could use somewhere between 40 and 1,000 cubic feet of gaseous carrier fluid for every gallon of liquid treatment agent. Using approximately 16,000 cubic feet of gaseous carrier fluid has been found to be very economical when compared to past processes for treating subterranean wells. It should be noted that the solution ratio can remain constant while the quantities of gaseous carrier fluid and liquid treatment agent increase or decrease in proportion to the characteristics of the petroleum bearing formation 36.

The chemical composition of the variety of components in the atomized treatment fog 38 enables the atomized treatment fog 38 to dissolve and shrink the clogging particles and/or swelled clays in the flow channels 18. The volume of atomized treatment fog 38 sprayed into the subterranean well 14 is based upon both the characteristics of the plurality of flow channels 18 and the subterranean well 14. The chemical reaction time necessary for the atomized treatment fog 38 to clear out the flow channels 18 is dependent upon the formation conditions in the subterranean well 14, including temperature, pressure, and number of flow channels 18.

In many instances, after the atomized treatment fog 38 is introduced into the subterranean well 14, the valve 26 is closed for a duration of time. This pressurizes the subterranean well 14 and ensures that the liquid treatment agent has adequate time to chemically react with particles and/or swelled clays that impede the flow channels 18. The duration of time should be at least one day but is typically between three and seven days. After enough time has lapsed, the valve 26 is opened to atmosphere (or tied into a gas gathering line) and the subterranean well 14 is brought back into production. Pressurizing the subterranean well 14 with the atomized treatment fog 38 has been found to be effective in subterranean wells 14 having low temperatures and petroleum bearing formations 36 with low pressures. In certain instances, the implementation of this treatment can increase the production rate of the subterranean well 14 by at least ten times the production rate before treatment. It should be understood that this process applies to any type of subterranean well, which include, but are not limited to, withdrawal wells, gas wells, and injection wells.

It has also been found that surfactant solutions comprising non-ionic ethoxylated sorbitan fatty acid esters also assist in decontaminating portions of the earth 40 that are contaminated with contaminating compounds. In such instances the surfactant solution is blended to an HLB that matches the contaminated portion of the earth 40. Then, in combination with the gaseous carrier fluid, the surfactant solution is pressured directly into the contaminated portions of the earth 40, where the surfactant solution energizes and lowers the viscosity of dissolved contaminating compounds. In effect, the treated contaminating compounds then become generally less resistant, making for easier removal from the earth. The contaminating compounds are then removed from the earth. In some instances the surfactant solution could be enhanced by having it diluted with solvents prior to being pressured directly into the contaminated portions of the earth 40. In other instances the surfactant solution can be used in conjunction with air when being pressured directly into the contaminated portions of the earth 40. It should be understood this contamination removal process can also be conducted in subterranean wells 14. Contaminating compounds include, but are not limited to, toxic chemicals, solvents, hydrocarbon solvents, and contaminants, etc.

This invention has been described with reference to several preferred embodiments. Many modifications and alterations will occur to others upon reading and understanding the preceding specification. It is intended that the invention be construed as including all such alterations and modifications in so far as they come within the scope of the appended claims or the equivalents of these claims. 

1: A process of treating a subterranean well comprising a plurality of flow channels, wherein at least one of the flow channels is impaired, the process treats the subterranean well by alleviating the impairment, the process comprising: identifying the specific characteristics of a petroleum bearing formation surrounding the subterranean well; creating a liquid treatment agent by: compounding a plurality of non-ionic ethoxylated sorbitan fatty acid ester surfactants together until a hydrophilic-lipophilic balance is achieved that matches the specific characteristics of the petroleum bearing formation surrounding the subterranean well, to create a surfactant solution; and subsequently diluting the surfactant solution with a solvent; supplying a continuous flow of gaseous carrier fluid into the subterranean well; allowing the gaseous carrier fluid to push any liquids out of the plurality of flow channels; atomizing the liquid treatment agent; blending the atomized liquid treatment agent with the gaseous carrier fluid to create an atomized treatment fog; and supplying the atomized treatment fog into the subterranean well. 2: The process of treating a subterranean well of claim 1 further comprising removing a portion of the liquids from the bottom of the subterranean well before supplying a continuous flow of gaseous carrier fluid into the subterranean well. 3: The process of treating a subterranean well of claim 1 further comprising: pressurizing the atomized treatment fog while in the subterranean well; allowing the pressurized atomized treatment fog to remain in the subterranean well for a duration of time; and allowing the subterranean well to depressurize such that the atomized treatment fog can escape. 4: The process of treating a subterranean well of claim 1 further comprising: pressurizing the atomized treatment fog while in the subterranean well; allowing the pressurized atomized treatment fog to remain in the subterranean well for between three and seven days; and allowing the subterranean well to depressurize such that the atomized treatment fog can escape. 5: The process of treating a subterranean well of claim 1 further comprising: placing a volume of the liquid treatment agent into a treatment supply tank; and providing the liquid treatment agent from the treatment supply tank to an atomizing apparatus. 6: The process of treating a subterranean well of claim 1 further comprising: placing a volume of the liquid treatment agent into a treatment supply tank; providing the liquid treatment agent from the treatment supply tank to an atomizing apparatus; atomizing the liquid treatment agent through the atomizing apparatus; and blending the atomized liquid treatment agent with the gaseous carrier fluid through the atomizing apparatus. 7: The process of treating a subterranean well of claim 1 further comprising compounding a sorbitan fatty acid ester with the surfactant solution until a hydrophilic-lipophilic balance is achieved that matches the specific characteristics of the petroleum bearing formation surrounding the subterranean well. 8: The process of treating a subterranean well of claim 1 further comprising enhancing the liquid treatment agent by adding inorganic acids, organic acids, clay stabilizers, bactericides, scale inhibitors, dissolved salts, emulsion breakers, water block breakers, or corrosion inhibitors. 9: The process of treating a subterranean well of claim 1 wherein the process is implemented through a gaseous carrier fluid atomizing system. 10: The process of treating a subterranean well of claim 1 wherein the surfactant solution is diluted with the solvent in a ratio of 1 part surfactant solution to 20 parts solvent. 11: The process of treating a subterranean well of claim 1 wherein the solvent is one of water, toluene, condensate, acetone, oils, mutual solvents, or a combination thereof. 12: The process of treating a subterranean well of claim 1 wherein the gaseous carrier fluid is air, natural gas, oxygen, propane, nitrogen, helium, carbon dioxide, or a combination thereof. 13: The process of treating a subterranean well of claim 1 wherein the atomized treatment fog comprising a solution ratio of between 100 and
 400. 14: The process of treating a subterranean well of claim 1 wherein the atomized treatment fog energizes and reduces the viscosity of any valuable liquids in the subterranean well. 15: The process of treating a subterranean well of claim 1 wherein the atomized treatment fog is supplied into the subterranean well as an aerosol mist. 16: A process of treating a subterranean well comprising a plurality of flow channels, wherein at least one of the flow channels is impaired, the process treats the subterranean well by alleviating the impairment, the process comprising: identifying the specific characteristics of a petroleum bearing formation surrounding the subterranean well; creating a liquid treatment agent by: compounding a plurality of non-ionic ethoxylated sorbitan fatty acid ester surfactants together until a hydrophilic-lipophilic balance is achieved that matches the specific characteristics of the petroleum bearing formation surrounding the subterranean well, to create a surfactant solution; and subsequently diluting the surfactant solution with a solvent; placing a volume of the liquid treatment agent into a treatment supply tank; supplying a continuous flow of gaseous carrier fluid into the subterranean well; allowing the gaseous carrier fluid to push any liquids out of the plurality of flow channels; providing the liquid treatment agent from the treatment supply tank to an atomizing apparatus; atomizing the liquid treatment agent through the atomizing apparatus; blending the atomized liquid treatment agent with the gaseous carrier fluid to create an atomized treatment fog through the atomizing apparatus; supplying the atomized treatment fog into the subterranean well as an aerosol mist; pressurizing the atomized treatment fog while in the subterranean well; allowing the pressurized atomized treatment fog to remain in the subterranean well for a duration of time; and allowing the subterranean well to depressurize such that the atomized treatment fog can escape. 17: The process of treating a subterranean well of claim 16 further comprising removing a portion of the liquids from the bottom of the subterranean well before supplying a continuous flow of gaseous carrier fluid into the subterranean well. 18: The process of treating a subterranean well of claim 16 further comprising compounding a sorbitan fatty acid ester with the surfactant solution until a hydrophilic-lipophilic balance is achieved that matches the specific characteristics of the petroleum bearing formation surrounding the subterranean well. 19: The process of treating a subterranean well of claim 16 further comprising enhancing the liquid treatment agent by adding inorganic acids, organic acids, clay stabilizers, bactericides, scale inhibitors, dissolved salts, emulsion breakers, water block breakers, or corrosion inhibitors. 20: The process of treating a subterranean well of claim 16 wherein the process is implemented through a gaseous carrier fluid atomizing system. 21: The process of treating a subterranean well of claim 16 wherein the surfactant solution is diluted with the solvent in a ratio of 1 part surfactant solution to 20 parts solvent. 22: The process of treating a subterranean well of claim 16 wherein the solvent is one of water, toluene, condensate, acetone, oils, mutual solvents, or a combination thereof. 23: The process of treating a subterranean well of claim 16 wherein the gaseous carrier fluid is air, natural gas, oxygen, propane, nitrogen, helium, carbon dioxide, or a combination thereof. 24: The process of treating a subterranean well of claim 16 wherein the atomized treatment fog comprising a solution ratio of between 100 and
 400. 25: The process of treating a subterranean well of claim 16 wherein the atomized treatment fog energizes and reduces the viscosity of any valuable liquids in the subterranean well. 26: A process of treating contaminated portions of the earth with a surfactant solution, the process comprising: creating surfactant solution by compounding a non-ionic ethoxylated sorbitan fatty acid ester surfactant with another surfactant until a proper hydrophilic-lipophilic balance is achieved; pressured the surfactant solution into the contaminated portions of the earth; allowing the surfactant solution to energize and reduce the viscosity of the contaminating compounds in the contaminated portions of the earth; and removing the contaminating compounds treated with the surfactant solution from the portions of the earth. 27: The process of treating contaminated portions of the earth of claim 26 further comprising enhancing the surfactant solution with solvents before injecting the surfactant solution into the contaminated portions of the earth. 28: The process of treating contaminated portions of the earth of claim 26 wherein the contaminating compounds are toxic chemicals, solvents, hydrocarbon solvents, or contaminants. 29: The process of treating a subterranean well of claim 1 wherein the specific characteristics identified is the hydrophilic-lipophilic balance of the petroleum bearing formation surrounding the subterranean well. 30: The process of treating a subterranean well of claim 16 wherein the specific characteristics identified is the hydrophilic-lipophilic balance of the petroleum bearing formation surrounding the subterranean well. 